CN106178557A - A kind of vertical tube falling vaporizer - Google Patents
A kind of vertical tube falling vaporizer Download PDFInfo
- Publication number
- CN106178557A CN106178557A CN201610763627.1A CN201610763627A CN106178557A CN 106178557 A CN106178557 A CN 106178557A CN 201610763627 A CN201610763627 A CN 201610763627A CN 106178557 A CN106178557 A CN 106178557A
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- Prior art keywords
- heat exchanger
- housing
- tube
- plate
- catheter
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/06—Evaporators with vertical tubes
- B01D1/065—Evaporators with vertical tubes by film evaporating
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
Abstract
The present invention relates to a kind of vertical tube falling vaporizer, including upper tube box, lower tube box, housing, many heat exchanger tubes, upper perforated plate and lower perforated plate, described upper tube box is provided with solution inlet port and indirect steam outlet I, lower tube box is provided with concentrated solution outlet and indirect steam outlet II, the top of described housing is provided with steam inlet, and the bottom of housing is provided with condensation water out；The film-distributing device for solution being laid in heat exchanger tube inwall it is provided with inside described upper tube box；Described film-distributing device includes liquid-bearing plate, feed liquor plate, liquid distribution plate and catheter；The present invention utilizes the stripping effect that indirect steam produces with liquid film, increases driving force of heat transfer and evaporation efficiency；This film-distributing device can make liquid film be uniformly distributed, and film forming is stable, it is to avoid dry wall phenomenon, makes the internal indirect steam response rate produced of vaporizer high, and it is convenient to reclaim, and improves heat transfer efficiency.
Description
Technical field
The present invention relates to falling film evaporation technical field, a kind of vertical tube falling vaporizer.
Background technology
Existing vaporizer is mainly used to realize the evaporation and concentration of feed liquid, is very typical chemical engineering unit operation in industry
Equipment, is widely used in the commercial production such as chemical industry, light industry, food, pharmacy, desalinization, sewage disposal.Existing vaporizer
General based on horizontal tube falling film and VERTICAL TUBE falling liquid film, wherein vertical tube falling vaporizer is usually and adds pan feeding in evaporation chamber
Liquid, solution passes through film-distributing device, is assigned in each heat exchanger tube, is membranaceous flowing downward along heat exchanger tube inwall, in film like
During feed solution flow, feed liquid is vaporized by the vapours heating that adds of heat exchanger tube outer wall, forms concentrated solution and indirect steam.Fall
Film evaporator is that the feed liquid of film evaporation device is heated by the vapours that adds utilizing pipe outer wall, the therefore work of falling film evaporator
Efficiency and service behaviour both depend on the distribution of liquid material.But traditional vertical tube falling evaporation equipment, many employing Multi-layer sprinkling dishes
During the operation of formula distributor, feed liquid has in the most lacunary distribution grid from what the top of feed tube entrance tube sheet was installed, utilizes material
The action of gravity of liquid itself flows downward so that the liquid material redistribution by Multi-layers distributing plate.Fall on the upper surface of tube sheet, material
Hydrorrhea flows to inside heat exchanger tube, is finally membranaceous flowing down at heat exchanger tube inwall, and the indirect steam produced is drawn by bottom.Equipment
It is frequently present of the shortcomings such as liquid film film-formation result is poor, condensate film stability is the highest, affects heat transfer efficiency；Steam with in membranaceous dirty
Liquid is discharged from bottom in heat exchanger tube jointly, underuses the stripping effect of steam；The additionally thermal source of evaporation and concentration operation
Mainly use the raw steam of boiler endlessly.Material low for concentration, that treating capacity is big, the energy that steam expends is quite may be used
Seeing, for needing the enterprise of outsourcing steam, along with the rise of market steam price, steam operating cost is more and more higher, enterprise
Burden be increased dramatically.How to improve stabilization of equipment performance, heat transfer efficiency, the operating cost of minimizing device steam, save the energy be
The difficult point of vaporizer design at present.
Summary of the invention
In order to improve stabilization of equipment performance, heat transfer efficiency, operating flexibility, the operating cost of minimizing device steam, joint further
The about energy, the present invention provides a kind of vertical tube falling vaporizer.
For solving above-mentioned technical problem, the technical solution used in the present invention is:
A kind of vertical tube falling vaporizer, including upper tube box, lower tube box, housing, many heat exchanger tubes, upper perforated plate and lower perforated plate, housing
Upper end be tightly connected with upper tube box, the lower end of housing is tightly connected with lower tube box；The upper end of housing is provided with upper perforated plate, housing
Lower end is provided with on lower perforated plate, upper perforated plate and lower perforated plate and is respectively equipped with multiple installing hole for installing heat exchanger tube, many heat exchanger tubes
It is that array is vertically installed between upper perforated plate and lower perforated plate by installing hole, close between the outer wall of heat exchanger tube with corresponding installing hole
Envelope is installed, and the upper end of heat exchanger tube communicates with upper tube box, and the lower end of heat exchanger tube communicates with lower tube box, and described upper tube box is provided with solution
Import and indirect steam outlet, lower tube box is provided with concentrated solution outlet and indirect steam outlet, the top of described housing is provided with steaming
Vapor inlet, the bottom of housing is provided with condensation water out；It is provided with inside described upper tube box for solution being laid in heat exchanger tube inwall
Film-distributing device；Described film-distributing device includes liquid-bearing plate, feed liquor plate, liquid distribution plate and catheter, and liquid-bearing plate is positioned at solution inlet port
Lower section, and be fixed on upper tube box inwall, the center of liquid-bearing plate is provided with the air rising hole for discharging indirect steam, feed liquor plate with
Cavity between upper tube box inwall forms solution and flows into the passage of liquid distribution plate, liquid distribution plate is uniformly provided with multiple for flowing to
Solution spraying to upper perforated plate upper surface and the liquid distributing hole of catheter outer surface, liquid distribution plate be provided with for catheter run through logical
Hole, the arrangement of catheter is identical with heat exchanger tube, and catheter one end is stretched into inside heat exchanger tube, and catheter and the center of heat exchanger tube
On same axis, between catheter outer surface with corresponding heat exchanger tube inwall, form cloth film annular space.
It is enlarging that described catheter stretches into the part in heat exchanger tube, and the spacing of enlarging and heat exchanger tube inwall is 1.5-
2.5mm。
The outer wall of described catheter is provided with spiral grooves.
Described spiral grooves is a plurality of, is arranged on position that catheter matches with heat exchanger tube or is arranged on catheter enlarging
Top.
Described indirect steam exportsExport with indirect steamIt is equipped with wire mesh demister.
It is between upper end and the upper tube box of described housing and between the lower end of housing and lower tube box and removably connects.
The external diameter of described upper perforated plate and lower perforated plate is all higher than the external diameter of housing, and the upper end of housing is by upper perforated plate and is located at
The connection bump of bobbin carriage outer wall uses securing memberIt is connected；The lower end of housing is by lower perforated plate and is located on lower tube box outer wall
Connection bump uses securing memberIt is connected.
It is provided with multiple deflection plate in described housing, and multiple deflection plate wherein side is all connected with inner walls, opposite side
And the S-shaped arrangement in gap formed between housing.
It is additionally provided with journal stirrup on described housing exterior walls.
Air rising hole on described liquid-bearing plate is tubular, and the top of air rising hole is higher than solution inlet port.
Beneficial effects of the present invention:
The vertical tube falling vaporizer that the present invention provides, during work, tube side fluid is flowed into the space on liquid-bearing plate top by solution inlet port,
Then solution uniformly flows into liquid distribution plate by the cavity formed between feed liquor plate and bobbin carriage inwall, finally keeps certain liquid level.
Solution is by the liquid distributing hole in upper liquid distribution plate, and uniformly spray is to upper perforated plate upper surface and catheter outer surface, it is ensured that each heat exchanger tube
Uniform liquid inventory；Arrangement mode that catheter is identical with heat exchanger tube and the enlarging of catheter tail end ensure that the residence of catheter
Neutral；Cloth film annular space, the enlarging of catheter tail end and the existence of spiral grooves formed between catheter with corresponding heat exchanger tube,
Make solution under the constraint with catheter outer wall of the heat exchanger tube inwall, be membranaceous flowing at heat exchanger tube internal face, it is achieved heat exchanger tube
The purpose of inwall uniform cloth film.Liquid film is vaporized by the vapours heating that adds of heat exchanger tube outer wall during flowing downward, and is changing
Inside heat pipe produce indirect steam, so rise steam with in membranaceous dirty liquid in heat exchanger tube counter current contacting generation vapour
Put forward effect, increase driving force of heat transfer and evaporation efficiency；Additionally indirect steam is carried secretly in passing through wire mesh demister removal steam
Discharged by upper and lower two indirect steams outlet after liquid foam and other impurity, it is ensured that the higher indirect steam response rate, after filtration
Indirect steam raw steam can be replaced to use as heat-source Cycles, thus reduce the demand of the energy to external world, operating cost is low, grasps
Stablize；
Liquid-bearing plate structure ensure that tube side fluid is flowed into the requisite space on liquid-bearing plate top by solution inlet port, it is to avoid solution is from leading
Liquid pipe upper port flows into inside catheter, ensure that indirect steam is arranged smoothly by the tubular air rising hole on liquid-bearing plate top simultaneously
Go out, improve the indirect steam response rate；The cavity passage formed between feed liquor plate and bobbin carriage inwall ensure that solution uniformly flows into
Liquid distribution plate；The liquid distributing hole of liquid distribution plate ensure that each heat exchanger tube liquid film flow, controls the descending liquid density of equipment；Cloth film annular space is protected
Demonstrate,prove liquid to be retrained by heat exchanger tube inwall and catheter outer wall, be membranaceous flowing at heat exchanger tube internal face；Catheter and heat exchange
The enlarging managing identical arrangement mode and catheter end ensure that the placed in the middle of catheter；Multichannel spiral grooves, increases molten
The disturbance of liquid, the thickness of thinning liquid film, reduces heat transmission resistance；The stripping effect that indirect steam produces with liquid film, increases heat transfer
Motive force and evaporation efficiency；This film distribution structure can make liquid film be uniformly distributed, and film forming is stable, it is to avoid dry wall phenomenon, makes vaporizer
The internal indirect steam response rate produced is high, and it is convenient to reclaim, and improves heat transfer efficiency.
Accompanying drawing explanation
Fig. 1 is present configuration schematic diagram；
Fig. 2 is the A direction view of Fig. 1；
Fig. 3 is the section B-B view of Fig. 1；
Fig. 4 is enlarged drawing at the C of Fig. 1；
Fig. 5 is that heat exchanger tube is connected figure with catheter；
Reference: 1, upper tube box, 2, solution inlet port, 3, indirect steam outlet, 4, liquid-bearing plate, 5, feed liquor plate, 6, catheter,
7, liquid distribution plate, 8, securing member, 9, upper perforated plate, 10, steam inlet, 11, housing, 12, heat exchanger tube, 13, deflection plate, 14, journal stirrup,
15, water out is condensed, 16, lower perforated plate, 17, securing member, 18, lower tube box, 19, concentrated solution outlet, 20, indirect steam outlet,
21, wire mesh demister, 22, air rising hole, 23, liquid distributing hole, 24, enlarging, 25, spiral grooves, 26, cloth film annular space.
Detailed description of the invention
Below in conjunction with detailed description of the invention, the present invention is further elaborated.
A kind of vertical tube falling vaporizer, including upper tube box 1, lower tube box 18, housing 11, many heat exchanger tubes 12, upper perforated plate 9 and
Lower perforated plate 16, the upper end of housing 11 is tightly connected with upper tube box 1, and the lower end of housing 11 is tightly connected with lower tube box 18；Housing 11
Upper end be provided with upper perforated plate 9, the lower end of housing be provided with on lower perforated plate 16, upper perforated plate 9 and lower perforated plate 16 be respectively equipped with multiple for
Installing the installing hole of heat exchanger tube 12, many heat exchanger tubes 12 are that array is vertically installed at upper perforated plate 9 and lower perforated plate 16 by installing hole
Between, seal between the outer wall of heat exchanger tube 12 with corresponding installing hole and install, and the upper end of heat exchanger tube 12 communicates with upper tube box 1,
The lower end of heat exchanger tube 12 communicates with lower tube box 18, and described upper tube box 1 is provided with solution inlet port 2 and indirect steam outlet3, lower tube box
18 are provided with concentrated solution outlet 19 and indirect steam outlet20, the top of described housing 11 is provided with steam inlet 10, housing 11
Bottom is provided with condensation water out 15；The internal cloth film dress being provided with for solution being laid in heat exchanger tube 12 inwall of described upper tube box 1
Put；Described film-distributing device includes liquid-bearing plate 4, feed liquor plate 5, liquid distribution plate 7 and catheter 6, and liquid-bearing plate 4 is positioned at solution inlet port 2
Lower section, and be fixed on upper tube box 1 inwall, the center of liquid-bearing plate 4 is provided with the air rising hole 22 for discharging indirect steam, feed liquor plate
Cavity between 5 and upper tube box 1 inwall forms solution and flows into the passage of liquid distribution plate 7, liquid distribution plate 7 is uniformly provided with multiple for inciting somebody to action
The solution spraying flow to is to upper perforated plate 9 upper surface and the liquid distributing hole 23 of catheter 6 outer surface, and liquid distribution plate 7 is provided with for drain
The through hole that pipe 6 runs through, the arrangement of catheter 6 is identical with heat exchanger tube 12, and it is internal that heat exchanger tube 12 is stretched in catheter 6 one end, and drain
The center of pipe 6 and heat exchanger tube 12 is on same axis, is formed between catheter 6 outer surface with corresponding heat exchanger tube 12 inwall
Cloth film annular space；It is enlarging 24 that described catheter 6 stretches into the part in heat exchanger tube 12, and the spacing of enlarging 24 and heat exchanger tube 12 inwall
For 1.5-2.5mm；The outer wall of described catheter 6 is provided with spiral grooves 25；Described spiral grooves 25 is a plurality of, is arranged on drain
Position that pipe 6 matches with heat exchanger tube 12 or be arranged on above the enlarging 24 of catheter 6；Described indirect steam exports3 and secondary
Steam (vapor) outlet20 are equipped with wire mesh demister 21；Between upper end and the upper tube box 1 of described housing 11 and housing 11 lower end with
It is between lower tube box 18 and removably connects；The external diameter of described upper perforated plate 9 and lower perforated plate 16 is all higher than the external diameter of housing 11, housing
The upper end of 11 uses securing member by upper perforated plate 9 and the connection bump being located at upper tube box 1 outer wall8 are connected；The lower end of housing 11
Securing member is used by lower perforated plate 16 and the connection bump being located on lower tube box 18 outer wall17 are connected；Set in described housing 11
There is multiple deflection plate 13, and multiple deflection plate 13 wherein side is all connected with housing 11 inwall, formed between opposite side and housing 11
The S-shaped arrangement in gap；It is additionally provided with journal stirrup 14 on described housing 11 outer wall；Air rising hole 22 on described liquid-bearing plate 4 in tubular, and
The top of air rising hole 22 is higher than solution inlet port 2, it is ensured that the liquid flowed into from solution inlet port, is introduced into the space on liquid-bearing plate top,
Avoiding flowing into inside catheter, the indirect steam that solution boils produces simultaneously is discharged by indirect steam outlet by air rising hole.
Fig. 1 show a kind of vertical tube falling evaporation structure schematic diagram, and bobbin carriage fluid is flowed into liquid-bearing plate 4 by solution inlet port 2
With in the space of air rising hole 22 formation, then the cavity by being formed between feed liquor plate 5 and upper tube box 1 inwall uniformly flows into cloth liquid
On plate 7, finally keep certain liquid level.Solution by the liquid distributing hole 23 in liquid distribution plate 7, uniformly spray to upper perforated plate 9 upper surface and
Catheter 6 outer surface.The cloth film annular space 26 that heat exchanger tube 12 and catheter 6 are formed, solution is again through cloth film annular space 26, enlarging 24, spiral shell
The common effect of rotation groove 25, flows down in the most membranaceous at heat exchanger tube 12 inwall.Liquid film flow downward during by heat exchange
Pipe 12 outer wall add vapours heating produce vaporization, so rising steam with in membranaceous dirty liquid in heat exchanger tube 12 inverse
Stream contact produces stripping effect, increases driving force of heat transfer and evaporation efficiency.Part indirect steam rises through catheter 6 and rises
Pore 22, enters upper tube box 1, by indirect steam outlet 3 discharge；Part indirect steam enters lower tube box 18 by secondary with concentrated solution
Steam (vapor) outlet 20 is discharged；Indirect steam removes, by wire mesh demister 21, the liquid foam and other impurity carried secretly in steam before discharging.
Indirect steam after filtration can replace raw steam to be entered by the steam inlet 10 on the top of evaporator shell 11 as heat source
Enter enclosure interior.So indirect steam entrance vaporizer replaces raw steam to use as heat-source Cycles, thus reduces and to external world can
The demand in source, operating cost is low, stable operation.
The stripping effect that unique film-distributing device and indirect steam and liquid film produce makes liquid film be uniformly distributed, and film forming is stable,
Avoiding dry wall phenomenon, improve the internal indirect steam response rate produced of vaporizer, it is convenient to reclaim, and heat transfer efficiency is high.
Fig. 1 ~ 5 are the specific embodiment of a kind of vertical tube falling vaporizer, have that liquid film profiling-quality is high, fluid infusion uniformly, become
Film is stable, operating flexibility is big, pressure difference value is little, high heat transfer coefficient, the indirect steam response rate high, power consumption is little, heat-source Cycles
The advantages such as use.Can be as a kind of high-efficiency evaporating concentration technique at chemical industry, light industry, food, pharmacy, desalinization, sewage
The commercial production such as reason are applied.
Claims (10)
1. a vertical tube falling vaporizer, including upper tube box (1), lower tube box (18), housing (11), many heat exchanger tubes (12), on
Tube sheet (9) and lower perforated plate (16), the upper end of housing (11) is tightly connected with upper tube box (1), the lower end of housing (11) and lower tube box
(18) it is tightly connected；The upper end of housing (11) is provided with upper perforated plate (9), and the lower end of housing is provided with lower perforated plate (16), upper perforated plate (9) and
Be respectively equipped with multiple installing hole for installing heat exchanger tube (12) on lower perforated plate (16), many heat exchanger tubes (12) by installing hole in
Array is vertically installed between upper perforated plate (9) and lower perforated plate (16), close between the outer wall of heat exchanger tube (12) and corresponding installing hole
Envelope is installed, and the upper end of heat exchanger tube (12) communicates with upper tube box (1), and the lower end of heat exchanger tube (12) communicates with lower tube box (18), its
It is characterised by: described upper tube box (1) is provided with solution inlet port (2) and indirect steam outlet(3), lower tube box (18) is provided with concentrated solution
Outlet (19) and indirect steam outlet(20), the top of described housing (11) is provided with steam inlet (10), the bottom of housing (11)
It is provided with condensation water out (15)；Described upper tube box (1) is internal is provided with the cloth film for solution is laid in heat exchanger tube (12) inwall
Device；Described film-distributing device includes liquid-bearing plate (4), feed liquor plate (5), liquid distribution plate (7) and catheter (6), and liquid-bearing plate (4) is positioned at
The lower section of solution inlet port (2), and be fixed on upper tube box (1) inwall, the center of liquid-bearing plate (4) is provided with for discharging indirect steam
Air rising hole (22), cavity between feed liquor plate (5) and upper tube box (1) inwall forms solution and flows into the passage of liquid distribution plate (7), cloth
Multiple solution spraying for flowing to it is uniformly provided with to upper perforated plate (9) upper surface and catheter (6) outer surface on liquid plate (7)
Liquid distributing hole (23), liquid distribution plate (7) is provided with for catheter (6) through hole that runs through, the arrangement of catheter (6) and heat exchanger tube (12)
Identical, it is internal that heat exchanger tube (12) is stretched in catheter (6) one end, and the center of catheter (6) and heat exchanger tube (12) is in same
On axis, between catheter (6) outer surface with corresponding heat exchanger tube (12) inwall, form cloth film annular space.
2. vertical tube falling vaporizer as claimed in claim 1, it is characterised in that: described catheter (6) stretches into heat exchanger tube (12)
Interior part is enlarging (24), and the spacing of enlarging (24) and heat exchanger tube (12) inwall is 1.5-2.5mm.
3. vertical tube falling vaporizer as claimed in claim 2, it is characterised in that: the outer wall of described catheter (6) is provided with spiral shell
Rotation groove (25).
4. vertical tube falling vaporizer as claimed in claim 3, it is characterised in that: described spiral grooves (25) is a plurality of, arranges
The position that catheter (6) matches with heat exchanger tube (12) or be arranged on catheter (6) enlarging (24) top.
5. vertical tube falling vaporizer as claimed in claim 1, it is characterised in that: described indirect steam exports(3) steam with secondary
Vapor outlet(20) wire mesh demister (21) it is equipped with.
6. vertical tube falling vaporizer as claimed in claim 1, it is characterised in that: the upper end of described housing (11) and upper tube box
(1) it is between and between the lower end of housing (11) and lower tube box (18) and removably connects.
7. vertical tube falling vaporizer as claimed in claim 1, it is characterised in that: described upper perforated plate (9) and lower perforated plate (16)
External diameter is all higher than the external diameter of housing (11), and the upper end of housing (11) is passed through upper perforated plate (9) and is located at the connection of upper tube box (1) outer wall
Protruding employing securing member(8) it is connected；The lower end of housing (11) is by lower perforated plate (16) and is located on lower tube box (18) outer wall
Connection bump uses securing member(17) it is connected.
8. vertical tube falling vaporizer as claimed in claim 1, it is characterised in that: described housing is provided with multiple deflection plate in (11)
(13), and multiple deflection plate (13) wherein side is all connected with housing (11) inwall, between being formed between opposite side and housing (11)
The S-shaped arrangement of gap.
9. vertical tube falling vaporizer as claimed in claim 1, it is characterised in that: it is additionally provided with journal stirrup on described housing (11) outer wall
(14).
10. vertical tube falling vaporizer as claimed in claim 1, it is characterised in that: the air rising hole (22) on described liquid-bearing plate (4)
In tubular, and the top of air rising hole (22) is higher than solution inlet port (2).
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| CN201610763627.1A CN106178557B (en) | 2016-08-30 | 2016-08-30 | A kind of vertical tube falling evaporator |
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|---|---|---|---|
| CN201610763627.1A CN106178557B (en) | 2016-08-30 | 2016-08-30 | A kind of vertical tube falling evaporator |
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| Publication Number | Publication Date |
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| CN106178557A true CN106178557A (en) | 2016-12-07 |
| CN106178557B CN106178557B (en) | 2018-07-06 |
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Cited By (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107281770A (en) * | 2017-07-28 | 2017-10-24 | 佛山德众制药机械有限公司 | A kind of controllable water-locator and use its falling film concentration machine |
| CN107308670A (en) * | 2017-07-16 | 2017-11-03 | 苏州卓群钛镍设备有限公司 | A kind of liquid guide flow distribution head |
| CN107362560A (en) * | 2016-12-30 | 2017-11-21 | 华北水利水电大学 | Falling film evaporator in the two phase countercurrent flow vertical tube of surrounding tangential admission |
| CN108088123A (en) * | 2017-12-15 | 2018-05-29 | 珠海格力电器股份有限公司 | A kind of liquid distributing pan structure, evaporator and air conditioner |
| CN108379859A (en) * | 2018-01-15 | 2018-08-10 | 浙江工业大学 | A kind of vertical tube high-efficiency falling film evaporation device |
| CN109157856A (en) * | 2018-09-25 | 2019-01-08 | 上海三耕储节能环保科技有限公司 | Film tube type falling film evaporator |
| CN109458773A (en) * | 2018-12-17 | 2019-03-12 | 江苏世林博尔制冷设备有限公司 | A kind of downward film evaporator bidirectional-reflux pipeline |
| CN109589626A (en) * | 2018-12-21 | 2019-04-09 | 江南大学 | Good antiscale property falling film evaporator |
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Cited By (18)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107362560A (en) * | 2016-12-30 | 2017-11-21 | 华北水利水电大学 | Falling film evaporator in the two phase countercurrent flow vertical tube of surrounding tangential admission |
| CN107308670B (en) * | 2017-07-16 | 2023-08-15 | 苏州卓群钛镍设备有限公司 | Liquid diversion distribution head |
| CN107308670A (en) * | 2017-07-16 | 2017-11-03 | 苏州卓群钛镍设备有限公司 | A kind of liquid guide flow distribution head |
| CN107281770A (en) * | 2017-07-28 | 2017-10-24 | 佛山德众制药机械有限公司 | A kind of controllable water-locator and use its falling film concentration machine |
| CN108088123A (en) * | 2017-12-15 | 2018-05-29 | 珠海格力电器股份有限公司 | A kind of liquid distributing pan structure, evaporator and air conditioner |
| CN108379859A (en) * | 2018-01-15 | 2018-08-10 | 浙江工业大学 | A kind of vertical tube high-efficiency falling film evaporation device |
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